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公开(公告)号：US3778971A
公开(公告)日：1973-12-18
申请号：US3778971D
申请日：1971-09-29
Applicant: RHONE POULENC SA
CPC classification number: B01D19/0031 , A61M5/36 , A61M2205/7527 , A61M2205/7536
Abstract: A device for purging gas bubbles from a liquid in which a wall is arranged to form a passageway, at least half of the wall being in the form of a hydrophobic porous membrane having a pore size between 0.01 to 30 Mu . The liquid flows parallel to the membrane in a passageway between 0.5 and 10 mm maximum thickness and the gas escapes through the pores. The membrane may be formed into a tube and may act as a connector between two lengths of piping, the gas escaping between the ends of the piping. In another construction the device is in the form of a sachet having an intermediate impermeable wall, the liquid being caused to flow parallel to the sides of the wall of the sachet.
Abstract translation: 一种用于从其中布置壁以形成通道的液体中吹扫气泡的装置，所述壁的至少一半为孔径为0.01至30μm的疏水性多孔膜形式。 液体在最大厚度为0.5至10毫米的通道中平行于膜流动，气体通过孔逸出。 膜可以形成为管，并且可以用作两段管道之间的连接器，气体在管道的端部之间逸出。 在另一种结构中，该装置是具有中间不可渗透壁的小袋形式，使液体平行于小袋的壁的侧面流动。
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2.发明授权
公开(公告)号：US3788474A
公开(公告)日：1974-01-29
申请号：US3788474D
申请日：1971-10-12
Applicant: RHONE POULENC SA
CPC classification number: A61M1/34 , A61M1/3403 , A61M1/341 , A61M2202/0401 , A61M2205/3331
Abstract: Apparatus and process for the concentration of a liquid containing non-ultrafiltrable elements, e.g. ascitic fluid in which liquid is fed to an ultrafilter having a membrane therein, and the concentrate and ultrafiltrate are withdrawn from the ultrafilter in which a pressure drop is induced in the concentrate by an auxiliary hydraulic resistance causing a pressure drop in concentrate which is proportional to the pressure drop exerted on the ultrafiltrate by the membrane in the inverse ratio to the ratio of the flow rates of the concentrate and of the ultrafiltrate.
Abstract translation: 用于浓缩含有非超滤元素的液体的装置和方法，例如， 其中液体被供给到其中具有膜的超滤器的腹水，并且浓缩物和超滤液从其中通过辅助液压阻力在浓缩物中引起压降的超滤器中取出，导致浓缩物的压降与成比例的 以膜的超滤液的压降与浓缩物和超滤液的流量的比率成反比。
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Patent Agency Ranking
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公开(公告)号：BE773201A
公开(公告)日：1972-03-28
申请号：BE773201
申请日：1971-09-28
Applicant: RHONE POULENC SA
Abstract: A device for purging gas bubbles from a liquid in which a wall is arranged to form a passageway, at least half of the wall being in the form of a hydrophobic porous membrane having a pore size between 0.01 to 30 mu . The liquid flows parallel to the membrane in a passageway between 0.5 and 10 mm maximum thickness and the gas escapes through the pores. The membrane may be formed into a tube and may act as a connector between two lengths of piping, the gas escaping between the ends of the piping. In another construction the device is in the form of a sachet having an intermediate impermeable wall, the liquid being caused to flow parallel to the sides of the wall of the sachet.
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公开(公告)号：SE375454B
公开(公告)日：1975-04-21
申请号：SE1226071
申请日：1971-09-28
Applicant: RHONE POULENC SA
Abstract: A device for purging gas bubbles from a liquid in which a wall is arranged to form a passageway, at least half of the wall being in the form of a hydrophobic porous membrane having a pore size between 0.01 to 30 mu . The liquid flows parallel to the membrane in a passageway between 0.5 and 10 mm maximum thickness and the gas escapes through the pores. The membrane may be formed into a tube and may act as a connector between two lengths of piping, the gas escaping between the ends of the piping. In another construction the device is in the form of a sachet having an intermediate impermeable wall, the liquid being caused to flow parallel to the sides of the wall of the sachet.
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公开(公告)号：GB1370629A
公开(公告)日：1974-10-16
申请号：GB4472771
申请日：1971-09-24
Applicant: RHONE POULENC SA
Abstract: 1370629 Degassing device with semipermeable membrane RHONE-POULENC SA 24 Sept 1971 [29 Sept 1970] 44727/71 Heading B1M A device for purging gas bubbles from a liquid comprises a wall defining a substantially unobstructed liquid passageway, at least 50% of the wall being in the form of a hydrophobic porous membrane, the pores of which have an apparent diameter of 0.01 to 30Á, the maximum thickness of the passageway, measured perpendicular to the porous membrane, being between 0.5 and 10 mm, the inner surface of the membrane having a critical surface tension of less than 40 dynes/om. at 20C. The terms "apparent diameter" and "critical surface tension" are defined in the Specification. The membrane may be formed from P.T.F.E., P.V.C., polyethylene, polyacrylonitrile which has been waterproofed, or paper formed from polynosic fibres. In Fig. 3, sheets 24 and 26 comprise micro porous P.V.C. of thickness 70Á with an average apparent diameter of 0.1Á reinforced with nylon 66 filament, and sheet 28 is of P.V.C. As liquid with bubbles enters at 32, passes through aperture 30 and then out at 34, gas bubbles in the liquid pass through walls 24 and 26. In the embodiment of Fig. 1 (not shown) the membrane is a tube which forms the passageway.
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